US5723164A - Thermostable edible composition having ultra-low water activity - Google Patents
Thermostable edible composition having ultra-low water activity Download PDFInfo
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- US5723164A US5723164A US08/668,931 US66893196A US5723164A US 5723164 A US5723164 A US 5723164A US 66893196 A US66893196 A US 66893196A US 5723164 A US5723164 A US 5723164A
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- cellulose
- filling
- thermostable
- surface area
- composition
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Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
- A23L29/20—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents
- A23L29/206—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of vegetable origin
- A23L29/262—Cellulose; Derivatives thereof, e.g. ethers
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- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
- A21D13/00—Finished or partly finished bakery products
- A21D13/30—Filled, to be filled or stuffed products
- A21D13/38—Filled, to be filled or stuffed products characterised by the filling composition
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P20/00—Coating of foodstuffs; Coatings therefor; Making laminated, multi-layered, stuffed or hollow foodstuffs
- A23P20/20—Making of laminated, multi-layered, stuffed or hollow foodstuffs, e.g. by wrapping in preformed edible dough sheets or in edible food containers
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P30/00—Shaping or working of foodstuffs characterised by the process or apparatus
- A23P30/20—Extruding
- A23P30/25—Co-extrusion of different foodstuffs
Definitions
- the invention relates to a thermostable edible composition having an ultra-low water activity. Specifically, the invention relates to a thermostable edible composition having an ultra-low water activity and containing an ultrahigh surface area particulate.
- the control of water activity in a food product can enable the food product to resist spoilage and maintain a fresh taste and mouth feel.
- the water activity of a food, or a food subsystem thereof is a useful measurement of the degree of "freeness" of water contained in that food. Water activity is determined by the combined effect of the moisture content of the food as well as the nature of various components dissolved in an aqueous phase of the food.
- the water activity (A w ) of a food is defined as the partial vapor pressure of water in the food divided by the saturation vapor pressure of pure water at the temperature of the food.
- the water activity of a food can be measured by placing a sample of the food to be tested in a container. The container is then sealed and the relative humidity above the sample is determined after equilibrium is reached.
- the relatively high water activities that are associated with fillings and cremes made by standard formulations, permit microbial growth, moisture migration, and other problems to occur in a food product.
- Fillings and cremes with high water activities are, essentially, a medium for supporting microbial growth and, therefore, have limited shelf lives.
- Fillings and cremes with high water activities generally, allow water to migrate into the surrounding foodstuff.
- the surrounding foodstuff is a material of significantly lower water activity, such as a baked dough, the migration of moisture into the baked dough makes the baked dough "soggy."
- Low water activities are, usually, required in baked doughs in order to maintain a crisp and crunchy texture.
- thermostable properties into fillings and other "food subsystems” often requires the use of stabilizers as flow control agents.
- Gums and other hydrocolloids are common stabilizers for aqueous food systems.
- Stabilizers provide flow control properties to aqueous food systems by altering the viscosity and texture of a food matrix.
- Stabilizers such as gums or hydrocolloids, generally, must be "activated” in the water or moisture content of such food systems in order to be effective. Many gums, even when activated, do not provide suitable thermostability to an aqueous food system because the stabilization properties of the gum are effected and altered by temperature. Fillings, that are stabilized by gums, often flow at temperatures that are commonly used during food preparation such as baking.
- a first group of gums form thermally irreversible gels.
- Thermally irreversible gels are useful in the preparation of "ovenable fillings" and are commonly prepared from high methoxy pectins. Thermally irreversible gels do not melt or flow unless they are exposed to temperatures that are significantly higher than the temperatures required for their original activation.
- a second group of gums alter the viscosity characteristics of an aqueous food system to render the aqueous food system essentially insensitive to temperature.
- An example of a viscosity altering gum is xanthan.
- Xanthan is a microbially-derived gum and provides viscosity properties to an aqueous food system.
- the viscosity properties are effected by stress or shear thinning rather than temperature.
- Viscosity altering gums provide an aqueous food system, such as fillings, that do not flow unless the temperature reaches the boiling point or the internal shear point of the aqueous food system.
- Gums and other hydrocolloids must remain activated within the water of an aqueous food system such as a filling.
- an aqueous food system must contain at least 20 percent moisture for these gums and hydrocolloids to remain activated.
- a gum or hydrocolloid is "activated" when it is in solution and functional. Therefore, gums and hydrocolloids are ineffectual as stabilizing agents in food systems that have moisture contents below about 15 percent.
- U.S. Pat. No. 4,037,000 to Burge et al. discloses an icing mixture.
- the icing mixtures of Examples 3 and 4 of the patent are compositions containing glycerol and aqueous xanthan. These compositions include glucose syrup and can contain from 6.0 to 10.5 percent by weight of free water.
- This patent does not disclose a thermostable creme having an ultra-low water activity.
- U.S. Pat. No. 4,670,272 to Chen et al. discloses a thermostable creme.
- the compositions of the creme of this patent can contain small concentrations of "polyols.”
- the compositions of this patent contain high fructose corn syrup or standard corn syrup and can contain cellulose products.
- the water activity of the creme of this patent is "low” or has an A w value of 0.6 to 0.7.
- the compositions of this patent are aerated cremes wherein modified starch is activated by cooking and provides the stabilizing and texturizing properties to the food system.
- the creme of this patent does not have an ultra-low moisture content, ultra-low water activity, or shelf life of 9 to 12 months.
- U.S. Pat. No. 4,752,494 to Tang et al. discloses a thermostable edible creme.
- the compositions of the creme of this patent can contain cellulose products, such as the AvicelTM product, and maltodextrin.
- the creme of this patent contains water from syrups or from water added to the creme. The added water can be in a concentration of up to 15 percent. Water must be present in a sufficient concentration to provide an "intermediate water activity base matrix" for calcium ions.
- the calcium ions and soluble caseinate of the creme of this patent stabilize and texturize the creme by forming a complexing gel between these two ingredients.
- the creme of this patent does not have an ultra-low moisture content, ultra-low water activity, or a shelf life of 9 to 12 months.
- U.S. Pat. No. 4,774,095 to Kleinschmidt et al. discloses filling-containing, dough-based products.
- This patent discloses an aqueous-based composition, but the composition combines glycerin with cellulose products.
- the preparation of this patent obtains a thermostable filling which uses defibrillated cellulose as a thixotropic flow control agent to obtain a relatively low viscosity.
- High-methoxy pectin is further employed, as a gelling hydrocolloid, to reduce the "stringiness" that is caused by the defibrillated cellulose and to establish a thermally irreversible matrix to prevent "boil-out" in the oven.
- the continuous phase of this filling is an aqueous sugar solution.
- the sugar solution must be selected so as to avoid crystallization that can result in an undesirable texture and "mouth feel.”
- the fillings of this patent have a water activity value below 0.5.
- the cellulose products, that are disclosed in this patent, are not "reactivated" in a non-aqueous polyol liquid in order to provide thermostability to the polyol liquid.
- U.S. Pat. No. 4,861,604 to Tang et al. describes a sheetable thermostable filling composition.
- the composition for the sheetable filling is applied in a thin laminate form.
- the functionality of the disclosed composition is provided by gelatin, maltodextrin, and pregelled starch.
- An intermediate preparation is critical to obtaining a low moisture content and water activity in the final baked product.
- the filling of this patent does not provide a multi-purpose thermostable filling having ultra-low water activity.
- thermostable edible composition that has an ultra-low moisture content, an ultra-low water activity, and a shelf life of at least nine months.
- the industry further lacks a thermostable filling that has these properties and a total lipid content of 15 percent or less.
- the edible composition of the invention includes a non-aqueous hydrophilic liquid and an ultrahigh surface area cellulose in sufficient quantity to heat stabilize the composition.
- the invention is, also, a method.
- the method includes mixing a non-aqueous hydrophilic liquid with a sufficient quantity of ultrahigh surface area cellulose into a slurry. Heating of the slurry is conducted to a temperature sufficient to activate the ultrahigh surface area cellulose. Shearing of the slurry then occurs until the ultrahigh surface area cellulose is reactivated.
- the invention includes thermostable fillings, that contain the invented composition, and methods for using the composition in a food.
- the edible composition of the invention includes a non-aqueous hydrophilic liquid and an ultrahigh surface area cellulose in sufficient quantity to heat stabilize the composition.
- the invented composition is thermostable and has an ultra-low water activity.
- the thermostable filling of this invention provides a "composite food subsystem” or filling for a foodstuff.
- composite food subsystem refers to fillings and also includes cremes, laminates, toppings, and the similar compositions.
- Thermostable fillings can be either sweet or savory and are particularly useful in the production of filled bakery products such as cookies, pretzels, pastries, bread sticks, and crackers.
- Thermostable fillings, according to this invention can also be used in other non-dough-based products such as filled confections having creme centers, taffy's, and caramels.
- the ultra-low water activity of the thermostable filling of this invention is at least below 0.6.
- the ultra-low water activity of desirable embodiments of the invented filling is below 0.5.
- the water activity of the preferred embodiment of the filling is between 0.15 and 0.45.
- thermostable filling having an ultra-low water activity
- These methods involve filling or otherwise combining an uncooked dough or confection food with the thermostable filling and, then, cooking the combined food system.
- the thermostability of the filling enables the filling to withstand high temperatures of baking, frying, or extruding without losing its texture or exhibiting "boil-out" during the cooking process.
- Desirable embodiments of the method of this invention provide multi-layered and multi-textured food compositions wherein the outer layers are a bakery dough. These embodiments desirably, but not exclusively, include methods of co-extruding or co-laminating the combined food subsystems.
- the final ready-to-eat products of these methods have long shelf lives of at least nine months because the low water activity of the filling (1) minimizes microbial problems and (2) maintains a crisp texture in adjacent food subsystems.
- the invented edible composition that provides the base of the filling, has a feel and consistency of fat and has a very low water activity or A w value as low as 0.15. Where it is desirable to raise the water activity of the final product, limited amounts of moisture can be added to the continuous liquid phase. A saturated solution of a sweetener, for example, is desirable for this purpose. Furthermore, it is often desirable to add an edible solid phase to the continuous phase of a filling in amounts up to 75 percent based on the weight of the continuous phase.
- the edible solid phase is most commonly a fine or "fondant quality" powder.
- the edible solid phase is, desirably, a member selected from the group consisting of flavoring materials, flavoring agents, taste modifiers, colorants, and other "functional ingredients", and mixtures of these. Other functional ingredients include buffer systems. Buffer systems can be added to the filling to impart desirable taste and textural properties.
- the ultrahigh surface area cellulose in a thermostable filling provides an effective flow control agent and provides the filling with its thermostable properties.
- Ultrahigh surface area cellulose can be prepared by a variety of processes from cellulose.
- Cellulose comprises primary linear chains of beta 1-4 D-glucopyranose units with an arrangement of secondary chains of beta 1-4 D-glucose to form an aggregate molecule.
- the primary linear chains within this aggregate molecule can be arrayed in a very ordered manner, such as a parallel or an anti-parallel manner.
- the primary linear chains can be arrayed in other complex structures including random structures.
- the secondary structure chains of cellulose are known as "microfibrils" and often, also, form a tertiary structure in the aggregate molecule. Therefore, regions of varying crystalline cellulose structures can be dispersed between or among regions of amorphous cellulose.
- cellulose structures such as bundles, sheets, and the like can form a tertiary structure of cellulose.
- This tertiary structure of cellulose is commonly known as a fibril or a fiber.
- the application of high shear to cellulose causes defibrillation of the cellulose.
- the defibrillation of the cellulose results in the distention and dislocation of microfibrils from the surface of the tertiary structures.
- This distention and dislocation of microfibrils expands or creates a hairy assemblage of microfibrils. It is believed that these exposed microfibrils cause the fibrils to adhere together and to form a network.
- the microfibrillular surface area of the network simultaneously exposes an extensive amount of hydroxyl groups.
- the hydroxyl groups can provide a high degree of inter-particle association and a substantial amount of hydrogen bonding between the fibrils and microfibrils throughout a hydrophilic continuous phase of a filling.
- the edible composition of this invention is made by reactivating an "ultrahigh surface area cellulose" or "USAC” in a non-aqueous hydrophilic liquid.
- An ultrahigh surface area cellulose is provided by first processing a selected cellulose to "activate” or expand its surface area. This first activation, typically, occurs in water and develops a sufficient particulate surface area in the cellulose to permit the cellulose to function as a stabilizer.
- the selection of a cellulose for use as the ultrahigh surface area cellulose can be performed by a viscosity test procedure.
- the viscosity test procedure for selecting an ultrahigh surface area cellulose is performed on a cellulose-gel of the sample of cellulose.
- the cellulose-gel can be prepared from a slurry or a powder of the sample of cellulose as follows.
- the selected sample of cellulose slurry or cellulose powder is to be adjusted so as to provide a cellulose-gel sample for use in the viscosity test procedure.
- the viscosity test procedure uses a sample of cellulose-gel that is prepared by either the procedure of Table 1 or of Table 2 as described above.
- the viscosity test procedure is as follows.
- the average value of the viscosity of the selected cellulose-gel sample is used to evaluate the suitability of the cellulose as an ultrahigh surface area cellulose.
- the average value of the viscosity of the selected ultrahigh surface area cellulose must be sufficient to heat stabilize a selected edible non-aqueous hydrophilic liquid in order for the cellulose to function as an ultrahigh surface area cellulose.
- the average value of the viscosity of the ultrahigh surface area cellulose is at least about 250 centipoise.
- the preferred viscosity of the selected ultrahigh surface area cellulose is about 1100 centipoise.
- a desirable ultrahigh surface area cellulose has a viscosity between about 250 centipoise and about 1950 centipoise.
- the edible composition of this invention has a concentration of ultrahigh surface area cellulose that is sufficient to provide a surface area of a fibril and microfibril network to thermostabilize an edible non-aqueous hydrophilic liquid phase.
- the surface area of the fibril and microfibril network is, desirably, at least 100 square meters per gram (m 2 /gm). More desirably, the total surface area of the ultrahigh surface area cellulose, when reactivated in an edible non-aqueous hydrophilic liquid, is in range from about 100 to about 200 m 2 /gm. This relatively large surface area is important to the flow control properties of the edible composition or a filling made from the edible composition.
- the surface area of a selected ultrahigh surface area cellulose can be measured using a Quantasorb instrument.
- This instrument is manufactured by the Quantachrome Company, Syosset, N.Y.. This instrument performs a monolayer nitrogen adsorption analysis of a prepared, dried sample of the ultrahigh surface area cellulose. This analysis is explained in the manual by Dawes, Biological Techniques for Transmission & Scanning Electron Microscopy, 2nd ed. (1979), 231-239.
- the desired surface areas of ultrahigh surface area cellulose are, typically, provided in concentrations of about 0.20 percent to about 4.0 percent by weight of an ultrahigh surface area cellulose in the composition.
- concentration of a selected ultrahigh surface area cellulose, that is sufficient to heat stabilize an edible non-aqueous hydrophilic liquid, is effected by the "functionality" of the ultrahigh surface area cellulose.
- the functionality of an ultrahigh surface area cellulose is determined by its surface area. An estimation as to whether the surface area of a cellulose sample is sufficient to function in this invention is provided by the average viscosity of the cellulose sample as explained above. Therefore, as the surface area of a cellulose increases, the concentration of the ultrahigh surface area cellulose, that is required to provide thermostability to an edible non-aqueous hydrophilic liquid, decreases.
- a sufficient network of fibrils and microfibrils of ultrahigh surface area cellulose causes the invented filling to be thixotropic.
- the ultrahigh surface area cellulose in the absence of mechanical shear, forms a cohesive mesh with the filling.
- This structural entanglement or mesh imparts a very high resting viscosity to the filling.
- This high resting viscosity is not significantly reduced until the temperature of the filling is elevated to the boiling point of the filling.
- this network resists or prevents flow of the filling during heating operations such as baking, frying, or extruding.
- Moderate mechanical shear in contrast, disrupts this cohesive mesh of the filling of the invention and lowers the viscosity of the filling.
- the shear forces generated during mastication are sufficient to disrupt this network. Mastication of the filling lowers the viscosity of the filling and disperses it rapidly in the mouth. This rapid, fluid dispersion provides a flavor release from the filling and creates an organoleptic sensation of moistness.
- the thixotropic cohesive network of ultrahigh surface area cellulose is composed, essentially, of water insoluble colloidal size particles of fibrils and microfibrils. This assemblage of fibrils and microfibrils functions as a water insoluble hydrocolloid stabilizer. In contrast, all other gums and hydrocolloids are, essentially, water soluble and require dissolution in water for activation of their stabilization properties.
- the independence of ultrahigh surface area cellulose from water for its activation properties provides thermostability to a filling having a very low moisture content. This property is identified as "reactivation" and is performed in the edible non-aqueous hydrophilic liquid.
- the continuous liquid phase of the invented filling desirably, includes other hydrophilic liquids which can facilitate hydrogen bonding within the invented composition of non-aqueous hydrophilic liquid and ultrahigh surface area cellulose.
- the presence of another hydrophilic liquid in the invented filling facilitates thermostability of the filling and permits the filling to remain, essentially, water-free.
- Ultrahigh surface area cellulose can be prepared by a number of processes.
- a specific source of an ultrahigh surface area cellulose, that is suitable for use with this invention, is derived from a cellulose product that is a member selected from the group consisting of microfibrillated cellulose, microreticulated microcrystalline cellulose, parenchymal cell cellulose, bacterial cellulose, and mixtures of these.
- Other sources of ultrahigh surface area cellulose can also be used for this invention.
- Microfibrillated cellulose (“MFC”) is produced from a low solids liquid suspension of regular cellulose pulp.
- a slurry of pulp is heated to a temperature of, desirably, at least 80° C. and passed through a commercially available APV Gaulin homogenizer that applies pressures of, preferably, between 5,000 to 8,000 pounds per square inch (psi).
- psi pounds per square inch
- the suspension is subjected to a high viscosity shearing action followed by a high viscosity decelerating impact against a solid surface.
- the high viscosity shearing action and decelerating impact are both caused by an instantaneous drop in pressure or "explosive decompression”.
- This process is repeated until the slurry of pulp becomes a substantially stable suspension.
- the stable suspension results from the development of an ultrahigh surface area. This process converts cellulose into microfibrillated cellulose without substantial chemical change to the cellulose starting material.
- Microreticulated microcrystalline cellulose (“MRMCC”) is produced from a low solids aqueous suspension of microcrystalline cellulose.
- Microreticulated microcrystalline cellulose is commercially available from the FMC Corporation under the trade name "Avacel PH101".
- the aqueous suspension of microcrystalline cellulose is passed through a commercially available APV Rannie homogenizer.
- the homogenizer applies super pressures of at least 12,000 psi and, preferably, at least 13,500 psi.
- the aqueous microcrystalline cellulose dispersion is subjected to the same high shear zone conditions as described above for the explosive decompression. This homogenization process is repeated until an aqueous dispersion of porous microreticulated microcrystalline cellulose particles, having the required ultrahigh surface area, is generated.
- Parenchymal cell-containing products such as spent sugar, beet pulp, and citrus juice sacs, are materials used for the preparation of parenchymal cell cellulose ("PCC"). Parenchymatous tissues possess unique morphologies and the cellulose structure contained within such cells is a tertiary structure resulting from intermeshed and relatively disordered layers of microfibrils of cellulose. Acidic or basic hydrolysis, elevated reaction temperature, and physical shearing can be combined to disrupt the intercellular organization of the parenchymal cell cellulose and to induce defibrillation of the membrane. The dissolution of pectin and arabinogalactan from the insoluble parenchymal cell cellulose occurs without substantial degradation of these compounds. This solid/liquid mass is separated by washing. The separation provides a parenchymal cell cellulose network having the required ultrahigh surface area characteristics.
- Bacterial fermentation of a sugar-containing solution can synthesize cellulose of high purity.
- Desirable bacteria for this purpose include the Acetobacter species.
- Subelementary fibrils are extruded from a row of pores in the bacterial cell.
- Each microfibril is composed of an average of three subelementary fibrils which are arrayed in a helix.
- Individual ribbons are composed of bundles of microfibrils that associate with one another by hydrogen bonding to form a tertiary structure. The width of this ribbon is significantly less than that of conventional cellulose fibers from plants.
- the pellicle/ribbon matrix of the Acetobacter exhibits substantial hydrophilicity due to its extensive interior surface area.
- the network of bacterial fibrils and microfibrils can be suitable for use with this invention in its native state. However, the total surface area of these fibrils and microfibrils can be significantly enhanced by high shear processing.
- the dilute aqueous ultrahigh surface area cellulose slurries that are produced by the processes above, generally contain less than 10 percent cellulose solids. Dehydration of the "activated" ultrahigh surface area cellulose slurries must be performed without hardening the cellulose solids so that the ultrahigh surface area cellulose can be redispersed without loss of its viscosity or other properties. The redispersion of the ultrahigh surface area cellulose into an edible non-aqueous hydrophilic liquid is identified as the "reactivation" of the ultrahigh surface area cellulose.
- Desirable insulators include polyhydroxy compounds. Desirable polyhydroxy compounds include carbohydrates or carbohydrate-related compounds such as sugars, oligosaccharides, starches, carbohydrate gums, and cellulose gums. The selection of an insulator depends on a number of factors including its solubility, drying characteristics, application characteristics, and cost. Medium conversion (“42DE”) corn syrups have been found to be particularly desirable insulators for use with the invention.
- the use of conventional spray drying and other drying processes can effectively dry a slurry of ultrahigh surface area cellulose.
- the ratio of the concentration of insulator to the concentration cellulose solids increases, the redispersion properties of the dried product are enhanced.
- Full reactivation of dehydrated ultrahigh surface area cellulose to approximately 100 percent of its original viscosity requires an insulator concentration of 100 percent to 200 percent based on the weight of the ultrahigh surface area cellulose. Therefore, the preferred dried ultrahigh surface area cellulose composition for this invention contains two-thirds medium conversion (“42DE”) corn syrup and one-third ultrahigh surface area cellulose as calculated on a dry solids basis.
- 42DE medium conversion
- the edible non-aqueous hydrophilic liquid is another component of the edible composition of this invention.
- Edible non-aqueous hydrophilic liquids for the purposes of this invention, contain less than 5 percent water. These liquids are considered to be "dry" liquids or essentially moisture-free liquids.
- Edible polyol humectants provide desirable non-aqueous hydrophilic liquids for the preparation of ultra-low water activity fillings according to this invention.
- a suitable edible polyol humectant is a member selected from the group consisting of glycerin, propylene glycol, 1,3-butylene glycol, and mixtures of these. Glycerin is the most preferred humectant for use with the invention because glycerin is commercially available in food grade or high purity concentrations and because glycerin has a low viscosity and a high boiling point.
- the amount of edible polyol humectant used in the continuous liquid phase is primarily dependent on the final water activity that is desired for the filling. Generally, the edible polyol humectant is at least 50 percent of the continuous liquid phase of the filing and can be up to 100 percent of the continuous liquid phase. When the edible polyol humectant is high purity glycerin, the boiling point of the filling exceeds 450° F. (232° C.) and the water activity is about 0.15. High purity glycerin is at least 99.5 percent pure.
- An-edible solid phase is, desirably, incorporated into the continuous liquid phase.
- the edible solid phase is desirably a fine fondant quality powder.
- the edible solid phase is, desirably, a member selected from the group consisting of sugar, maltodextrin, polydextrose, salt, and mixtures of these.
- a sugar is, desirably, a member selected from the group consisting of sucrose, dextrose, fructose, corn syrup solids, sorbitol, and mixtures of these.
- the edible solid phase can include an insoluble solid.
- a desirable insoluble solid is a member selected from the group consisting of powdered alpha-cellulose, calcium sulfate, and mixtures of these.
- Desirable concentrations of edible solid phase ingredients are from about 5 percent to about 75 percent by weight of the final filling and are, preferably, used in quantities of between about 33 percent or "one-third” and above 67 percent or "two-thirds" by weight of the final filling.
- Limited amounts of moisture can, optionally, be added to the a filling made with the edible composition of the invention when an elevated water activity is desired for the final product.
- an aqueous solution is, desirably, added to the continuous liquid phase.
- saturated syrups such as fruit juice concentrates, can also be added.
- Stabilizers in the form of water soluble gums can further be incorporated into the composition to prevent or retard syneresis. The most thermostable of such fillings have an ultra-low water activity of below 0.6.
- Flavoring materials, taste modifiers, colorants, and other "functional ingredients” can be added to the filling composition for the purpose of imparting desirable taste, appearance, and textural properties.
- Virtually any known flavoring material can be added to the filling.
- An example of a desirable flavoring material includes a member selected from the group consisting of cheese powder, cocoa powder, chocolate liquor, tomato powder, cinnamon, meat powder, dehydrated fruit pieces, dehydrated vegetable pieces, nuts, nut butter, cultured milk powder, and mixtures of these.
- Taste modifiers can be used in the filling composition to eliminate or reduce the sweetness intensity of glycerin or another polyol.
- An example of a taste modifier includes a member selected from the group consisting of sodium salt of paramethoxyphenoxypropionic acid (commercially available under trade name “Lactisole” from the Tate & Lyle), purified potassium salt of hop isohumulones (commercially trade name “Isolone” from Kalsec), and mixtures of these.
- An objective of the invention is to provide a fat-free thermostable filling, but the filling composition can include small amounts of fat and emulsifiers to modify the texture and improve the handling characteristics of a filling without the filling losing its desirable characteristics.
- Desirable fats are partially or fully hydrogenated.
- Unsaturated oils that can be hydrogenated and used with the invention include an oil that is a member selected from the group consisting of coconut oil, corn oil, soybean oil, cotton seed oil, and mixtures of these.
- a suitable emulsifier includes a member selected from the group consisting of lecithin, a mono-glyceride, a di-glyceride, sorbitan monostearate, and mixtures of these.
- the melting point of a fat generally varies according to the degree of saturation or hydrogenation of the fat.
- a fat having a "Wiley melting point” of about 80° F. to 112° F. (26° C. to 45°) is preferred.
- Coconut fat, having a Wiley melting point of 92° F. (33° C.) is the most preferred fat.
- the addition of fats and/or emulsifiers to the filling composition provides the filling with a desirable "shortness" and reduces the "stringiness" of the filling during processing.
- the concentration of fat added to the filling composition is, desirably, about 0 percent to 15 percent, based on the final weight of the filling. A more desirable concentration of fat is less than 10 percent.
- the preferred concentration of fat is less than 5 percent.
- An optional ingredient can be a member selected from the group consisting of natural colorant, synthetic colorant, an opacifier, vitamin, a mineral, a sequestrant, a buffer, an aeration agent, including a leavener such as sodium bicarbonate, a whipping aid, including egg white and soy albumin, and mixtures of these.
- the invention includes a method for making the edible composition as well as methods for making a thermostable filling having ultra-low water activity from the edible composition.
- the method optionally, includes mixing an edible non-aqueous hydrophilic liquid, which is desirably glycerin, with any saturated solution to adjust a water activity value for the edible non-aqueous hydrophilic liquid and the saturated solution to a desired value.
- the method further involves mixing any hydrophilic continuous liquid phase component with the edible non-aqueous hydrophilic liquid and, optionally, the saturated solution to form a slurry.
- the mixing procedures are preferably, performed in a jacketed scrape surface kettle.
- the method then requires adding a sufficient quantity of ultrahigh surface area cellulose into the slurry.
- Heating of the slurry is then performed at a temperature sufficient to reactivate the ultrahigh surface area cellulose in the edible non-aqueous hydrophilic liquid. Desirable temperatures are between about 120° F. and about 160° F. (about 49° C. and about 71° C.). The preferred temperature is 140° F. (60° C.). Shearing of the slurry then occurs, desirably, through an in-line high shear mixer or a homogenizer until the ultrahigh surface area cellulose is completely activated in the continuous phase. This procedure, typically, requires one to three sequential passes through the mixer or homogenizer. Essentially, full activation of the dry ultrahigh surface area cellulose must be achieved.
- thermostable filling containing a fat are performed by melting the fat and, then, mixing the fat into the slurry, desirably, with a portion of a solid powder phase.
- Aeration agents can, optionally, be pre-whipped into all or a portion of the original composition slurry of the hydrophilic continuous phase.
- thermostable filling made with the edible composition of the invention and a method for making the thermostable filling.
- the filling provided by this example is a thermostable, ultra-low water activity, fat-free, vanilla-flavored filling.
- the filling of this example is suitable for use with sandwich cookies such as those cookies sold under the trade name OREO.
- the glycerin is mixed in a scrape surface, jacketed kettle with the dried USAC stabilizer to form a slurry.
- This slurry is heated to 140° F. (60° C.) and then passed three times through an in-line high shear mixer.
- a MegatonTM brand slotted rotor/stator line-pressure mechanical homogenizer manufactured by Kinematic is used for this example.
- the shearing procedure is continued until the USAC is fully reactivated.
- the slurry is a continuous liquid phase having an appearance and a texture comparable to a soft fat.
- the remaining ingredients are then added to the kettle and the entire mixture is blended into a uniform slurry.
- the slurry is then cooled to ambient temperature to form the thermostable filling.
- the cooled, thermostable filling has an A w of 0.15 and a boiling point in excess of 450° F. (232° C.).
- thermostable filling made with the edible composition of the invention and a method for making the thermostable filling.
- the filling provided by this example is a thermostable, ultra-low water activity, low-fat, cheese-flavored filling.
- the filling of this example is suitable for use with a savory-flavored, filled snack such as those sold under the trade name COMBO.
- the glycerin, along with the LactisoleTM solution, is mixed in a scrape surface, jacketed kettle with the dried USAC stabilizer to form a slurry.
- This slurry is heated to 140° (160° C.) and then passed three times through an in-line high shear mixer.
- a MegatonTM brand slotted rotor/stator line-pressure mechanical homogenizer manufactured by Kinematic is used for this example.
- the shearing procedure is continued until the USAC is fully reactivated.
- the slurry is a continuous liquid phase having an appearance and a texture comparable to a soft fat.
- the remaining ingredients are then added with mixing into the kettle and the entire mix is blended into uniform slurry.
- the slurry is then cooled to ambient temperature to form the thermostable filling.
- the cooled, thermostable filling has an A w of 0.25 and a boiling point of approximately 450° F. (232° C.).
- thermostable filling made with the edible composition of the invention and a method for making the thermostable filling.
- the thermostable filling provided by this example is a thermostable, ultra-low water activity, low-fat, chocolate-flavored filling.
- the filling of this example is suitable for use with filled cookies such as those cookies sold under the trade name MAGIC MIDDLES.
- the glycerin is mixed in a scrape surface, jacketed kettle with the dried USAC stabilizer to form a slurry.
- This slurry is heated to 140° F. (60° C.) and then passed three times through an in-line high shear mixer.
- a MegatonTM brand slotted rotor/stator line-pressure mechanical homogenizer manufactured by Kinematic is used for this example.
- the shearing procedure is continued until the USAC is fully reactivated.
- the slurry is a continuous liquid phase having an appearance and a texture comparable to a soft fat.
- the chocolate liquor is melted and added to the kettle with mixing.
- the remaining ingredients are than added to the kettle and the entire mixture is blended to a uniform slurry.
- the slurry is then cooled to ambient temperature to form the thermostable filling.
- the cooled, thermostable filling has an A w of about 0.15 and a boiling point in excess of 450° F. (232° C.).
- thermostable filling made with the edible composition of the invention and a method for making the thermostable filling.
- the filling provided by this example is a thermostable, ultra-low water activity, fat-free, vanilla-flavored filling.
- the filling of this example is suitable for use with sandwich cookies such as those cookies sold under the trade name OREO.
- the propylene glycol is mixed in a scrape surface, jacketed kettle with the dried USAC stabilizer to form a slurry.
- This slurry is heated to 160° F. (71° C.) and then passed three times through an in-line high shear mixer.
- a MegatonTM brand slotted rotor/stator line-pressure mechanical homogenizer manufactured by Kinematic is used for this example.
- the shearing procedure is continued until the USAC is fully reactivated.
- the slurry is a continuous liquid-phase having an appearance and a texture comparable to a soft fat.
- the remaining ingredients are then added to the kettle and the entire mixture is blended into a uniform slurry.
- the slurry is then cooled to ambient temperature to form the thermostable filling.
- the cooled, thermostable filling has an A w of 0.15 and a boiling point in excess of 450° F. (232° C.).
- thermostable filling of the invention The following is an example of the thermostable filling of the invention and the method for making the thermostable filling.
- the filling provided by this example is a thermostable, ultra-low water activity, fat-free, vanilla-flavored filling.
- the filling of this example is suitable for use with sandwich cookies such as those cookies sold under the trade name OREO.
- the 1,3-butylene glycol and the glycerin are mixed in a scrape surface, jacketed kettle with the dried USAC stabilizer to form a slurry.
- This slurry is heated to 130° F. (54° C.) and then passed three times through an in-line high shear mixer.
- a MegatonTM brand slotted rotor/stator line-pressure mechanical homogenizer manufactured by Kinematic is used for this example.
- the shearing procedure is continued until the USAC is fully reactivated.
- the slurry is a continuous liquid phase having an appearance and a texture comparable to a soft fat.
- the remaining ingredients are then added to the kettle and the entire mixture is blended into a uniform slurry.
- the slurry is then cooled to ambient temperature to form the thermostable filling.
- the cooled, thermostable filling has an A w of 0.15 and a boiling point in excess of 450° F. (232° C.).
- a co-extruded cookie composite is disclosed in this example that uses the thermostable filling of Example 3.
- the following standard sugar cookie formulation is the outer dough wrap.
- the softened butter, shortening, and sugar are mixed together in a Hobart mixer.
- the eggs are added in three stages with blending after each addition.
- the nonfat milk and vanilla are added with mixing.
- the cake flour is slowly added and blended on slow speed for 5 minutes.
- Example 3 and the cookie dough are fed into opposite sides of a Rheon Model KN100 co-extruder and formed. These compositions are fed to the co-extruder in a ratio of approximately 40 percent of the filling to 60 percent of the dough.
- the prebake cookie size is set at approximately 25 to 30 grams.
- the co-extruder is regulated using an inner setting of 22 and an outer setting of 30 to provide it with an uniform fill.
- the cookies are extruded in the shape of small balls and are flattened to provide a normal sugar cookie appearance.
- the cookies are baked at 400° F. (204° C.) for approximately 8 minutes.
- the "after bake" weight is about 25 grams. The cookies bake without leakage.
- thermostable filling that is prepared from the following formulation.
- the blending instructions to prepare the filling are the same as those described in Example 3 with the exception that Nulomcline® product is substituted for the glycerin.
- the filling has an A w of 0.60 to 0.65.
- the standard sugar cookie wrap described in Example 6 is also prepared for this comparative example.
- the filling and cookie dough are fed into opposite sides of a Rheon Model KN100 co-extruder and formed in the same procedure as described in Example 6, but using a higher water activity filling.
- the resulting cookie is approximately 40 percent filling and 60 percent dough and is formed by using an inner setting of 22 and an outer setting of 30 with an approximate prebake weight of 25 to 30 grams.
- the shape of the mass is that of small balls and the cookies are flattened to provide a normal sugar cookie appearance.
- the cookies are baked at 400° F. (204° C.) for approximately 8 minutes. The surface of the cookies crack open during baking and the filling leaks through the top of the cookies.
- This comparative example demonstrates that fillings having water activities higher than 0.60 are not suitable in the preparation of dual textured, cold formed, baked goods.
- a co-extruded cookie composite is disclosed in this example that uses the thermostable filling of Example 3 and the following low fat sugar cookie formulation as the outer dough wrap.
- KeliteTM CME is blended into the dry sugars.
- the butter, shortening, Dur Lo EmulisiferTM, and Nulomoline® are mixed with the sugar mixture in a Hobart mixer.
- the eggs are added in three stages with blending after each addition.
- Water is added in three stages with blending and mixed on medium speed for 5 minutes.
- the nonfat dry milk, Egg Shade, Butter Flavor, and vanilla are added with mixing.
- the cake flour is slowly added with mixing at slow speed for 5 minutes.
- Example 3 The cookie filling of Example 3 and the dough are fed into opposite sides of the Rheon Model KN100 co-extruder at a ratio of approximately 25 percent of filling and 75 percent of dough.
- the co-extruder is operated at an inner setting of 15 and an outer setting of 45.
- the prebake weight of the cookies is approximately 35 grams.
- the cookies are in the shape of small balls and are flattened to provide a normal sugar cookie appearance.
- the cookies are baked at 400° F. (204° C.) for approximately 8 minutes. The product bakes without any leakage.
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- Health & Medical Sciences (AREA)
- Dispersion Chemistry (AREA)
- Nutrition Science (AREA)
- Manufacturing & Machinery (AREA)
- Jellies, Jams, And Syrups (AREA)
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Abstract
Description
TABLE 4 ______________________________________ INGREDIENT WEIGHT ______________________________________ Glycerin.sup.1 100 lbs USAC Stabilizer, Dry.sup.2 3 lbs Sugar, Powdered.sup.3 200 lbs Vanillin Variable Total 303 lbs ______________________________________ .sup.1 The glycerin is 99.5 percent pure, food grade glycerin. .sup.2 The USAC is in a ratio of 33 percent "dry solids basis" and is an ultrahigh surface area cellulose known as microfibrillated cellulose. .sup.3 The sugar is a 6X food grade sugar without starch.
TABLE 5 ______________________________________ INGREDIENT WEIGHT ______________________________________ Glycerin.sup.1 100 lbs USAC Stabilizer, Dry.sup.2 3 lbs Cheese Powder.sup.3 100 lbs Maltodextrin.sup.4 88 lbs Salt, Microfine 12 lbs Lactisole ™.sup.5 300 ppm Flavor Variable Total 603 lbs ______________________________________ .sup.1 The glycerin is 99.5 percent pure, food grade glycerin. .sup.2 The USAC is in a ratio of 33 percent "dry solids basis" and is an ultrahigh surface area cellulose known as microfibrillated cellulose. .sup.3 The cheese powder is a commercially available high temperature cheddar powder. .sup.4 The maltodextrin is 10DE and 100 percent passes through a 200 U.S. mesh screen. .sup.5 The Lactisole ™ product is added as a 50 percent aqueous solution (41 grams Lactisole ™ product plus 41 grams water).
TABLE 6 ______________________________________ INGREDIENT WEIGHT ______________________________________ Glycerin.sup.1 100 lbs USAC Stabilizer, Dry.sup.2 3 lbs Sugar, Powdered.sup.3 80 lbs Chocolate Liquor 20 lbs Natural Flavors Variable Total 203 lbs ______________________________________ .sup.1 The glycerin is 99.5 percent pure, food grade glycerin. .sup.2 The USAC is in a ratio of 33 percent "dry solids basis" and is an ultrahigh surface area cellulose known as microfibrillated cellulose. .sup.3 The sugar is a 6X food grade sugar without starch.
TABLE 7 ______________________________________ INGREDIENT WEIGHT ______________________________________ Propylene Glycol.sup.1 100 lbs USAC Stabilizer, Dry.sup.2 3 lbs Sugar, Powdered.sup.3 200 lbs Vanillin Variable Total 303 lbs ______________________________________ .sup.1 The propylene glycol is 99.5 percent pure, food grade. .sup.2 The USAC is in a ratio of 33 percent "dry solids basis" and is an ultrahigh surface area cellulose known as parenchymal cell cellulose. .sup.3 The sugar is a 6X food grade sugar without starch.
TABLE 8 ______________________________________ INGREDIENT WEIGHT ______________________________________ 1,3-Butylene Glycol.sup.1 50 lbs Glycerin.sup.1 50 lbs USAC Stabilizer, Dry.sup.2 3 ibs Sugar, Powdered.sup.3 200 lbs Vanillin Variable Total 303 lbs ______________________________________ .sup.1 The 1,3butylene glycol and the glycerin are 99.5 percent pure, foo grade. .sup.2 The USAC is in a ratio of 33 percent "dry solids basis" and is an ultrahigh surface area cellulose known as microreticulated microcrystalline cellulose. .sup.3 The sugar is a 6X food grade sugar without starch.
TABLE 9 ______________________________________ INGREDIENT CONCENTRATION ______________________________________ Cake Flour 43.0% Shortening 25.0% Granulated Sugar 10.0% Powdered Sugar 10.0% Whole Eggs 5.2% Butter 5.0% Nonfat Dry Milk 1.4% Vanilla 0.4% Total 100.0% ______________________________________
TABLE 10 ______________________________________ INGREDIENT WEIGHT ______________________________________ Nulomoline ®.sup.1 120 lbs USAC Stabilizer Dry.sup.2 3 lbs Sugar, Powdered.sup.3 60 lbs Chocolate Liqueur 20 lbs Natural Flavors Variable Total 203 lbs ______________________________________ .sup.1 Nulomoline ® is a partial invert sugar syrup manufactured by Crompton & Knowles Corporation. .sup.2 The USAC is in a ratio of 33 percent "dry solids basis" and is an ultrahigh surface area cellulose known as microfibullated cellulose. .sup.3 The sugar is a 6X food grade sugar without starch.
TABLE 11 ______________________________________ INGREDIENT CONCENTRATION ______________________________________ Cake Flour 44.00% Water 10.00% Granulated Sugar 9.00% Powdered Sugar 8.95% Dur Lo Emulisifer ™.sup.1 5.20% Whole Eggs 5.20% Nulomoline ®.sup.2 5.00% Butter 5.00% Shortening 5.00% Nonfat Dry Milk 1.40% Kelit ™ CME.sup.3 0.80% Vanilla 0.04% Egg Shade DT901546.sup.4 0.04% Butter Flavor C10,860.sup.5 0.01% Total 100.00% ______________________________________ .sup.1 Dur Lo Emulisifer ™ is manufactured by Van Den Bergh Foods. .sup.2 Nulmoline ® is a partial invert sugar syrup manufactured by Crompton & Knowles Corporation. .sup.3 Kelite ™ CME is xanthan gum manufactured by Kelco. .sup.4 Egg Shade DT901546 is a color solution manufactured by Crompton & Knowles Corporation. .sup.5 Butter Flavor C10,860 is an artificial butter flavor manufactured by Crompton & Knowles Corporation.
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US08/668,931 US5723164A (en) | 1993-01-13 | 1996-06-24 | Thermostable edible composition having ultra-low water activity |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/004,051 US5366750A (en) | 1993-01-13 | 1993-01-13 | Thermostable edible composition having ultra-low water activity |
US08/345,694 US5529801A (en) | 1993-01-13 | 1994-11-21 | Thermostable edible composition having ultra-low water activity |
US08/668,931 US5723164A (en) | 1993-01-13 | 1996-06-24 | Thermostable edible composition having ultra-low water activity |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US08/345,694 Continuation US5529801A (en) | 1993-01-13 | 1994-11-21 | Thermostable edible composition having ultra-low water activity |
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US5723164A true US5723164A (en) | 1998-03-03 |
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US08/345,694 Expired - Lifetime US5529801A (en) | 1993-01-13 | 1994-11-21 | Thermostable edible composition having ultra-low water activity |
US08/668,931 Expired - Fee Related US5723164A (en) | 1993-01-13 | 1996-06-24 | Thermostable edible composition having ultra-low water activity |
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US08/004,051 Expired - Lifetime US5366750A (en) | 1993-01-13 | 1993-01-13 | Thermostable edible composition having ultra-low water activity |
US08/345,694 Expired - Lifetime US5529801A (en) | 1993-01-13 | 1994-11-21 | Thermostable edible composition having ultra-low water activity |
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US (3) | US5366750A (en) |
EP (1) | EP0679062A4 (en) |
JP (1) | JPH09502861A (en) |
AU (1) | AU682496B2 (en) |
CA (1) | CA2153764C (en) |
WO (1) | WO1994015484A1 (en) |
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- 1993-01-13 US US08/004,051 patent/US5366750A/en not_active Expired - Lifetime
-
1994
- 1994-01-12 CA CA002153764A patent/CA2153764C/en not_active Expired - Fee Related
- 1994-01-12 AU AU62278/94A patent/AU682496B2/en not_active Ceased
- 1994-01-12 WO PCT/US1994/000174 patent/WO1994015484A1/en not_active Application Discontinuation
- 1994-01-12 EP EP94909432A patent/EP0679062A4/en not_active Withdrawn
- 1994-01-12 JP JP6516200A patent/JPH09502861A/en active Pending
- 1994-11-21 US US08/345,694 patent/US5529801A/en not_active Expired - Lifetime
-
1996
- 1996-06-24 US US08/668,931 patent/US5723164A/en not_active Expired - Fee Related
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Cited By (34)
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US6322829B1 (en) * | 1996-09-05 | 2001-11-27 | The Pillsbury Company | Savory fillings and food products including these fillings |
US5962059A (en) * | 1996-09-05 | 1999-10-05 | Nestec S.A. | Aerated lactic protein and crystallized fat food product and its preparation |
US6090428A (en) * | 1997-06-25 | 2000-07-18 | Joseph Ventura Rancho | Spreadable protein compositions |
EP1063897A1 (en) | 1998-03-18 | 2001-01-03 | Kal Kan Foods, Inc. | Multicomponent food product and methods of making and using the same |
US6146672A (en) * | 1998-04-02 | 2000-11-14 | The Pillsbury Company | Water-in-oil emulsion fillings |
US6183799B1 (en) * | 1999-05-27 | 2001-02-06 | Nestec S.A. | Extrusion process for laminated candy products |
US6623784B2 (en) | 2000-11-15 | 2003-09-23 | Nestec S.A. | Process for molding laminated candy and resultant products thereof |
US6592928B2 (en) | 2000-11-15 | 2003-07-15 | Nestec S.A. | Festooned laminated candy and methods for making same |
US6616963B1 (en) | 2000-11-15 | 2003-09-09 | Nestec S.A. | Laminated candy products made by an extrusion process |
US6689406B2 (en) | 2000-12-05 | 2004-02-10 | Nestec S.A. | Chocolate coating process and device for same |
US20040146660A1 (en) * | 2001-06-06 | 2004-07-29 | Goodwin Andrew James | Surface treatment |
US6805890B2 (en) | 2001-09-06 | 2004-10-19 | Nestec S.A. | Laminated, extruded candy products |
US20030054071A1 (en) * | 2001-09-06 | 2003-03-20 | William Wu | Extrusion apparatus for laminated candy products |
US7074446B2 (en) | 2003-10-30 | 2006-07-11 | Frito-Lay North America, Inc. | Method for making a dual-textured food substrate having large seasoning bits |
US20050095321A1 (en) * | 2003-10-30 | 2005-05-05 | Heywood Adrianna A. | Method for making a dual-textured food substrate having large seasoning bits |
US8216620B2 (en) | 2003-10-30 | 2012-07-10 | Frito-Lay North America, Inc. | Dual-textured food substrate having large seasoning bits |
US7569242B2 (en) | 2003-10-30 | 2009-08-04 | Frito-Lay North America, Inc | Snack food having large bits |
US20060115561A1 (en) * | 2003-10-30 | 2006-06-01 | Heywood Adrianna A | Method for making a dual-textured food substrate having large seasoning bits |
US20060115562A1 (en) * | 2003-10-30 | 2006-06-01 | Barber Keith A | Snack food having large bits |
US20050249845A1 (en) * | 2004-05-10 | 2005-11-10 | Mihalos Mihaelos N | Process for preparing filled cracker products |
WO2005117601A2 (en) * | 2004-06-03 | 2005-12-15 | General Mills Marketing, Inc. | Shaped cookie intermediates using bake stable fillings to form visual features |
WO2005117601A3 (en) * | 2004-06-03 | 2006-05-04 | Gen Mills Marketing Inc | Shaped cookie intermediates using bake stable fillings to form visual features |
US20050271785A1 (en) * | 2004-06-03 | 2005-12-08 | Hayes-Jacobson Susan M | Shaped cookie intermediates using bake stable fillings to form visual features |
US20090114624A1 (en) * | 2005-04-27 | 2009-05-07 | Honda Motor Co., Ltd. | Support structure for welding backbar |
US20070042099A1 (en) * | 2005-08-17 | 2007-02-22 | Stanton Robert P | Ready to bake refrigerated batter |
US20110183059A1 (en) * | 2005-08-17 | 2011-07-28 | Oven Luv'n Llc | Ready to bake refridgerated batter |
US9060531B2 (en) | 2007-10-31 | 2015-06-23 | Corporativo Internacional Mexicano, S. De R.L. De C.V. | Laminated baked snack bar |
US9119410B2 (en) | 2008-02-29 | 2015-09-01 | Intercontinental Great Brands Llc | Filled, baked crispy snack having a high moisture content |
US20100209588A1 (en) * | 2009-02-17 | 2010-08-19 | Kraft Foods Global Brands Llc | Bake-Stable Creamy Food Filling Base |
US8691316B2 (en) | 2009-02-17 | 2014-04-08 | Intercontinental Great Brands Llc | Bake-stable creamy food filling base |
US8287936B2 (en) | 2009-02-17 | 2012-10-16 | Kraft Foods Global Brands Llc | Bake-stable creamy food filling base |
US9456620B2 (en) | 2009-02-17 | 2016-10-04 | Intercontinental Great Brands Llc | Bake-stable creamy food filling base |
US20130266717A1 (en) * | 2010-12-15 | 2013-10-10 | Kraft Foods Global Brands Llc | Heat tolerant lipid-based filling |
US9351501B2 (en) * | 2010-12-15 | 2016-05-31 | Intercontinental Great Brands Llc | Heat tolerant lipid-based filling |
Also Published As
Publication number | Publication date |
---|---|
CA2153764C (en) | 2004-03-16 |
US5529801A (en) | 1996-06-25 |
WO1994015484A1 (en) | 1994-07-21 |
AU682496B2 (en) | 1997-10-09 |
EP0679062A1 (en) | 1995-11-02 |
JPH09502861A (en) | 1997-03-25 |
EP0679062A4 (en) | 1998-05-20 |
CA2153764A1 (en) | 1994-07-21 |
AU6227894A (en) | 1994-08-15 |
US5366750A (en) | 1994-11-22 |
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